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Getting Started with Chemcad
Creating flowsheets and running simulations is fast and easy with CHEMCAD, and the program is highly customizable to fit your needs and the way you work.
Before we start , should you know the basic procedure for creating a simulation that can be broken down into the following common steps:
1-Start new simulation
2-Select engineering units for the simulation.
3-Create a flow sheet
4-Select chemical components for the process.
5-Select K‐value and enthalpy options for the process.
6-Define the feed streams used in the process.
7-Enter specifications for the unit operations.
8-Run the simulation.
Let start with a simple example to show how you can applied previous procedure.
Example 1
A flash chamber operating 80oC(176oF)and 500kPa (72.5 psia)is separating 1000 kg/hr (2204 lb/hr) of a feed that is 10 mol%Ethane, 5%Propane, 15% n-Butane, 10% n-Pentane,12% iso-Pentane, 8% n-Hexane, 30%Heptane and 10%Nonane. What are the product compositions and flow rates? Feed conditions are the same as that of the flash chamber.
Solution Methodology
Step 1: After you Start up Chemcad , start new simulation, how?
Select File>>Save as, then name your simulation Flash Chamber. See pictures below.
Step 2: Now select engineering units that you will use for your simulation.
Select Format>>Engineering Unit>> Select default setting in English units.
Step3: Creat flowsheet
- First you need to select the piece(s) of equipment you desire, from All UnitOps tap select Feed arraw, two prodcut arraws and Flash #1.
Then select Stream to conect Flash with in and outputs arraws,after connecting press Ecs. -
Step 4: select chemical components for the process and here we have (Ethane, Propane, n-Butane, n-Pentane, iso-Pentane, n-Hexane, Heptane and Nonane), from toolbar select ,or select Thermophysical>>Select components..
from available component select desired components and then press
Step 5: Select K‐value and enthalpy options for the process, after selecting the desired components thermodynamic wizard window open to let the user enter pressure/temperature rang for the process or you can use the default rang, these input let the program choose the suitable thermodynamic models.
After press OK the program choose thermodynamic process for your process.
Press OK, and the program open a thermodynamic setting ,if you accept the default thermodynamic model by program press OK, if not change it, from global K values option select the thermodynamic model that you want, here want to chang SRK to Peng-Robinson.
Step 6: Define the feed streams, by double click on stream 1 entering to the flash separator, then enter the name to the stream optionally, specify temperature and pressure and the enthalpy and vapor fraction calculated automatically or specify pressure and vapor fraction and the enthalpy and temperature calculated and so on.
Episode 58 : Tools Integration Examples
* Separation of a binary mixture of Acetone-Chloroform (Determine the optimal separation scheme)
* Separation of the mixture components from the reactor effluent stream containing the reactants and products for esterification of methanol with acetic acid (Determine a feasible separation sequence)
SAJJAD KHUDHUR ABBAS
Ceo , Founder & Head of SHacademy
Chemical Engineering , Al-Muthanna University, Iraq
Oil & Gas Safety and Health Professional – OSHACADEMY
Trainer of Trainers (TOT) - Canadian Center of Human
Development
Episode 52 : Flow sheeting Case Study
A Standard Test Problem for Flowsheeting
The Cavett Problem
* A typical flowsheeting problem from the petroleum industry
* The flowsheet consists of mixers and TP-flash units
* The mixture consists of ethane, propane, 1- butane, n-butane, i-pentane, n-pentane
* The problem is interesting because tear-stream convergence is not easy and process is very sensitive to changes to the condition of operation
SAJJAD KHUDHUR ABBAS
Ceo , Founder & Head of SHacademy
Chemical Engineering , Al-Muthanna University, Iraq
Oil & Gas Safety and Health Professional – OSHACADEMY
Trainer of Trainers (TOT) - Canadian Center of Human
Development
The aim of this experiment is to determine the rheological properties of the mud by using model 900 viscometer.
1- Measuring mud viscosity (cp). That show the ability of the mud to caring cutting to the surface.
2- Measuring yield point. We was familiar with viscometer model 900
Getting Started with Chemcad
Creating flowsheets and running simulations is fast and easy with CHEMCAD, and the program is highly customizable to fit your needs and the way you work.
Before we start , should you know the basic procedure for creating a simulation that can be broken down into the following common steps:
1-Start new simulation
2-Select engineering units for the simulation.
3-Create a flow sheet
4-Select chemical components for the process.
5-Select K‐value and enthalpy options for the process.
6-Define the feed streams used in the process.
7-Enter specifications for the unit operations.
8-Run the simulation.
Let start with a simple example to show how you can applied previous procedure.
Example 1
A flash chamber operating 80oC(176oF)and 500kPa (72.5 psia)is separating 1000 kg/hr (2204 lb/hr) of a feed that is 10 mol%Ethane, 5%Propane, 15% n-Butane, 10% n-Pentane,12% iso-Pentane, 8% n-Hexane, 30%Heptane and 10%Nonane. What are the product compositions and flow rates? Feed conditions are the same as that of the flash chamber.
Solution Methodology
Step 1: After you Start up Chemcad , start new simulation, how?
Select File>>Save as, then name your simulation Flash Chamber. See pictures below.
Step 2: Now select engineering units that you will use for your simulation.
Select Format>>Engineering Unit>> Select default setting in English units.
Step3: Creat flowsheet
- First you need to select the piece(s) of equipment you desire, from All UnitOps tap select Feed arraw, two prodcut arraws and Flash #1.
Then select Stream to conect Flash with in and outputs arraws,after connecting press Ecs. -
Step 4: select chemical components for the process and here we have (Ethane, Propane, n-Butane, n-Pentane, iso-Pentane, n-Hexane, Heptane and Nonane), from toolbar select ,or select Thermophysical>>Select components..
from available component select desired components and then press
Step 5: Select K‐value and enthalpy options for the process, after selecting the desired components thermodynamic wizard window open to let the user enter pressure/temperature rang for the process or you can use the default rang, these input let the program choose the suitable thermodynamic models.
After press OK the program choose thermodynamic process for your process.
Press OK, and the program open a thermodynamic setting ,if you accept the default thermodynamic model by program press OK, if not change it, from global K values option select the thermodynamic model that you want, here want to chang SRK to Peng-Robinson.
Step 6: Define the feed streams, by double click on stream 1 entering to the flash separator, then enter the name to the stream optionally, specify temperature and pressure and the enthalpy and vapor fraction calculated automatically or specify pressure and vapor fraction and the enthalpy and temperature calculated and so on.
Episode 58 : Tools Integration Examples
* Separation of a binary mixture of Acetone-Chloroform (Determine the optimal separation scheme)
* Separation of the mixture components from the reactor effluent stream containing the reactants and products for esterification of methanol with acetic acid (Determine a feasible separation sequence)
SAJJAD KHUDHUR ABBAS
Ceo , Founder & Head of SHacademy
Chemical Engineering , Al-Muthanna University, Iraq
Oil & Gas Safety and Health Professional – OSHACADEMY
Trainer of Trainers (TOT) - Canadian Center of Human
Development
Episode 52 : Flow sheeting Case Study
A Standard Test Problem for Flowsheeting
The Cavett Problem
* A typical flowsheeting problem from the petroleum industry
* The flowsheet consists of mixers and TP-flash units
* The mixture consists of ethane, propane, 1- butane, n-butane, i-pentane, n-pentane
* The problem is interesting because tear-stream convergence is not easy and process is very sensitive to changes to the condition of operation
SAJJAD KHUDHUR ABBAS
Ceo , Founder & Head of SHacademy
Chemical Engineering , Al-Muthanna University, Iraq
Oil & Gas Safety and Health Professional – OSHACADEMY
Trainer of Trainers (TOT) - Canadian Center of Human
Development
The aim of this experiment is to determine the rheological properties of the mud by using model 900 viscometer.
1- Measuring mud viscosity (cp). That show the ability of the mud to caring cutting to the surface.
2- Measuring yield point. We was familiar with viscometer model 900
ECRIN SAPHIR TUTORIAL Dr. P. Ghahri Prepared by.docxtidwellveronique
ECRIN SAPHIR TUTORIAL
Dr. P. Ghahri
Prepared by: Amir Golparvar
[email protected]
Ecrin Saphir Tutorial
Initialization
This turotial is an introduction to the basic features of Saphir. It is assumed that you have installed Ecrin
workstation or Saphir stand alone to follow this session. The session can be followed in all levels of Saphir
except the Saphir reader.
The session will use the following files provided in the tutorial directory: SapGS01.rat, the rate file and
SapGS01.pre, the pressure file. The extension to the files is not important here as any ASCII file can be
loaded by the application.
Click on new project icon directly from toolbar.
This opens in succession two dialogs:
Ecrin Saphir Tutorial
This dialog allows you to choose the test type, reference fluid type, the available fluid rates, net drained
thickness, well radius and average porosity. Set the reference time to Dec 4, 1999 at 00:06:45 hours. Keep
all other parameters as the suggested default.
Click
You input the PVT characteristics; formation volumes factor, the fluid viscosity and the system
compressibility. Keep all values at their suggested defaults.
Click to create the new project. The Saphir main screen is displayed.
Ecrin Saphir Tutorial
The main screen is opened with the 'Interpretation' page active. This page (or panel) contains six icons
and by clicking consecutively on the icons from top to bottom, executing the dialogs and instructions, you
will follow exactly the default path of the basic workflow used in pressure transient analysis.
Loading Data
Click . This will initialize the load sequence which is normally a sequence of two dialogs. Specify
an ASCII file in the 'Define Data Source' dialog and click on to browse to the file SapGS01.rat in the
tutorial directory. A preview of the file will be shown in the dialog as illustrated in Figure below.
Ecrin Saphir Tutorial
Click to go to the Data Format dialog. Saphir has recognized the file as valid and has
automatically assigned the first column as 'Decimal Time' and the second as 'Oil Rate'. This is known as
'free format'. The units are correct so no need to change the formatting proposed by Saphir. See Figure
Below.
Ecrin Saphir Tutorial
Click on to load the flow rate file. A history plot with the loaded flowrate file in steps is
displayed. Double click in the title bar of the plot to maximize it and display the scales.
A click on the time button in the time scale will change the scale to real time (ToD) as
defined with the reference date and time at startup. Minimize the plot.
Ecrin Saphir Tutorial
Loading Pressure Data
Click on the icon . This will initialize the load process. Specify an ASCII file in the 'Define Data
Source' dialog and click on to browse to the file SapGS01.pre in the tutorial directory. A preview of the file
will be shown in th.
Similar to Easy thermodynamics calculations with Simulis Thermodynamics from ProSim (20)
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The alleged breach affected Europol agencies CCSE, EC3, Europol Platform for Experts, Law Enforcement Forum, and SIRIUS. Infiltration of these entities can disrupt ongoing investigations and compromise sensitive intelligence shared among international law enforcement agencies.
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Stay Informed on Threat Actors’ Activity on the Dark Web with SOCRadar!
Unleash Unlimited Potential with One-Time Purchase
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Enterprise Resource Planning System includes various modules that reduce any business's workload. Additionally, it organizes the workflows, which drives towards enhancing productivity. Here are a detailed explanation of the ERP modules. Going through the points will help you understand how the software is changing the work dynamics.
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